AU2964189A - Method for purifying high-temperature reducing gas - Google Patents

Method for purifying high-temperature reducing gas

Info

Publication number
AU2964189A
AU2964189A AU29641/89A AU2964189A AU2964189A AU 2964189 A AU2964189 A AU 2964189A AU 29641/89 A AU29641/89 A AU 29641/89A AU 2964189 A AU2964189 A AU 2964189A AU 2964189 A AU2964189 A AU 2964189A
Authority
AU
Australia
Prior art keywords
absorbent
reducing gas
regeneration
temperature reducing
regeneration step
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
AU29641/89A
Other versions
AU610337B2 (en
Inventor
Kenji Inoue
Makoto Kobayashi
Shigeaki Mitsuoka
Toshio Nakayama
Toru Seto
Hiromi Shirai
Mitsugi Suehiro
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Central Research Institute of Electric Power Industry
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from JP63027441A external-priority patent/JPH0790137B2/en
Priority claimed from JP63228383A external-priority patent/JPH0790140B2/en
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Publication of AU2964189A publication Critical patent/AU2964189A/en
Application granted granted Critical
Publication of AU610337B2 publication Critical patent/AU610337B2/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00—Purifying combustible gases containing carbon monoxide
    • C10K1/20—Purifying combustible gases containing carbon monoxide by treating with solids; Regenerating spent purifying masses
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/30—Sulfur compounds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/30—Sulfur compounds
    • B01D2257/304—Hydrogen sulfide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/40—Further details for adsorption processes and devices
    • B01D2259/40011—Methods relating to the process cycle in pressure or temperature swing adsorption
    • B01D2259/40058—Number of sequence steps, including sub-steps, per cycle
    • B01D2259/40064—Five
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/40—Further details for adsorption processes and devices
    • B01D2259/404—Further details for adsorption processes and devices using four beds

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Industrial Gases (AREA)
  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)
  • Silicon Compounds (AREA)
  • Manufacture Of Iron (AREA)
  • Cleaning Or Drying Semiconductors (AREA)

Abstract

In a method for absorbing and removing sulfur compounds such as hydrogen sulfide and carbonyl sulfide present in a high-temperature reducing gas using an absorbent, disclosed is a method for purifying a high-temperature reducing gas which is characterized in that: said method uses at least four towers of reactors filled with an absorbent and comprises four steps which are an absorption step for absorbing and removing sulfur compounds with an absorbent, a regeneration step for regenerating said absorbent using a gas containing oxygen, a cooling step after the regeneration step, and a reduction step for reducing said regenerated and cooled absorbent with a high-temperature reducing gas until the concentration of the reducing gas becomes uniform before and after passing through the absorbent; heat is continuously recovered from the high-temperature gas at the outlet of the regeneration reactor in said regeneration step; and the regeneration and absorption performance is thus stabilized. Also disclosed is a method for purifying a high-temperature reducing gas which is characterized in that this method uses at least four towers (16,17,18,19) filled with an absorbent as in the above method; and an additional preliminary regeneration step is provided besides the above four steps in order to make possible a smooth operation when switching to the regeneration step and the continuous recovery of sulfur.
AU29641/89A 1988-02-10 1989-02-06 Method for purifying high-temperature reducing gas Ceased AU610337B2 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP63-27441 1988-02-10
JP63027441A JPH0790137B2 (en) 1988-02-10 1988-02-10 Refining method for high temperature reducing gas
JP63-228383 1988-09-14
JP63228383A JPH0790140B2 (en) 1988-09-14 1988-09-14 Refining method for high temperature reducing gas

Publications (2)

Publication Number Publication Date
AU2964189A true AU2964189A (en) 1989-08-10
AU610337B2 AU610337B2 (en) 1991-05-16

Family

ID=26365355

Family Applications (1)

Application Number Title Priority Date Filing Date
AU29641/89A Ceased AU610337B2 (en) 1988-02-10 1989-02-06 Method for purifying high-temperature reducing gas

Country Status (7)

Country Link
US (1) US5154900A (en)
EP (1) EP0328479B1 (en)
CN (1) CN1010379B (en)
AT (1) ATE120480T1 (en)
AU (1) AU610337B2 (en)
CA (1) CA1324875C (en)
DE (1) DE68921905T2 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0817906B2 (en) * 1989-01-05 1996-02-28 三菱重工業株式会社 Sulfur recovery method in refining process of high temperature reducing gas
JP2865845B2 (en) * 1990-10-08 1999-03-08 三菱重工業株式会社 Purification method of high-temperature reducing gas
JP3831435B2 (en) * 1995-10-11 2006-10-11 三菱重工業株式会社 Gas purification equipment
JP4533515B2 (en) * 2000-08-16 2010-09-01 三菱重工業株式会社 Syngas production method
CN101880553B (en) * 2010-06-22 2013-03-13 沈阳航空航天大学 Integrated medium-high temperature coal gas purification method and device suitable for coal-based gas
CN103191677A (en) * 2013-04-26 2013-07-10 华东理工大学 Analog moving bed reactor and operating method and application thereof
CN105694989A (en) * 2016-02-03 2016-06-22 山东佳星环保科技有限公司 High-temperature coal gas purification technique
CN112226617A (en) * 2020-08-31 2021-01-15 宁波住铁精密机械有限公司 Copper smelting method for improving stability

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1822293A (en) * 1928-05-14 1931-09-08 Cie Int Fab Essences & Petrole Process for regenerating contaminated purifying agents
US2747968A (en) * 1951-05-07 1956-05-29 Pigache Pierre Gustave Adolphe Dry process for the recovery of sulfur from gases
US4164544A (en) * 1976-08-27 1979-08-14 United States Steel Corporation Desulfurization of hot reducing gas
US4371507A (en) * 1980-09-23 1983-02-01 Phillips Petroleum Company Catalytic hydrogenation of olefins, hydrodesulfurization of organic sulfur compounds and/or selective removal of hydrogen sulfide from fluid streams
JPS57184418A (en) * 1981-05-01 1982-11-13 Babcock Hitachi Kk Method for recovering sulfur in dry type flue gas desulfurizing apparatus
US4533529A (en) * 1983-10-21 1985-08-06 Standard Oil Company Sulfur recovery process

Also Published As

Publication number Publication date
DE68921905D1 (en) 1995-05-04
AU610337B2 (en) 1991-05-16
EP0328479A3 (en) 1990-10-10
EP0328479B1 (en) 1995-03-29
ATE120480T1 (en) 1995-04-15
EP0328479A2 (en) 1989-08-16
CN1037091A (en) 1989-11-15
DE68921905T2 (en) 1995-09-28
US5154900A (en) 1992-10-13
CN1010379B (en) 1990-11-14
CA1324875C (en) 1993-12-07

Similar Documents

Publication Publication Date Title
EP0212297B1 (en) High pressure process for sulfur recovery from a hydrogen sulfide containing gas stream
US4053554A (en) Removal of contaminants from gaseous streams
HU895832D0 (en) Method for removing and recovering sulfur dioxide from gases
AU2964189A (en) Method for purifying high-temperature reducing gas
KR970006836B1 (en) Process for removing h2s from a gas stream
EP0399608A3 (en) Process for removing acid gas from a gas mixture containing acid gas
AU625919B2 (en) Method for purifying high-temperature reducing gas
AU8466491A (en) Process for purifying high-temperature reducing gases
KR850006152A (en) Removal of sulfur compounds from exhaust gases
CA2006093C (en) Removing hydrogen sulphide from a gas mixture
JPS6411625A (en) Method for purifying high-temperature reductive gas
CA1149136A (en) Method for removing carbonyl sulfide in gas treating processes
JPH0776348B2 (en) Refining method for high temperature reducing gas
CA2118120A1 (en) Process and apparatus for recovering sulphur from a gas stream containing hydrogen sulphide
KR100405522B1 (en) How to exclude carbon dioxide capture in coke gas purification
Grunewald et al. Process for desulfurizing CO 2-containing gases
WO2001052974A1 (en) Method for removing sulfur compounds from gas mixtures
US4163776A (en) Process for stack gas desulfurization
CA1214625A (en) Process for removal of hydrogen sulfide and carbon dioxide from gas streams
JPS544871A (en) Simultaneous desulfurizing and denitrating method for exhaust gas
JPH02237613A (en) Method for refining high-temperature reducing gas
JPS56126428A (en) Dry type stack gas desulfurizing process
JPS63122790A (en) Purification of high-temperature reducing gas
JPS5851923A (en) Dry desulfurization of waste gas
JPS54150372A (en) Separating method for h2s and co2 from gas mixture selectively